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Process Equipment and Plant Design

Process Equipment and Plant Design
The safe height (h) to diameter (d) ratio (i.e., h/d) for liquid/petro fuel storage tank of capacity more than 45 kilolitres is less than

3
3.5
1
2

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Process Equipment and Plant Design
Vertical vessels are not supported by

Saddles
Columns
Brackets
Skirts

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Process Equipment and Plant Design
With increase in pressure drop (for a given particle size), the dust collection efficiency of a cyclone separator will

Increase
Remain unaffected
Increase or decrease depending on the nature of the dust
Decrease

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Process Equipment and Plant Design
The ratio of the largest load in a test to the original cross-sectional area of the test specimen is called the __________ stress.

Ultimate
None of these
Breaking
Yield point

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Process Equipment and Plant Design
A perforated plate has holes of diameter dh arranged in a pitch ph. Each hole has a tube of I.D. dt passing through it. The ligament efficiency is given by

(ph - dh)/ph
(ph - dh)/dh
(ph - dh . dt/2)/ph
(ph - dt)/ph

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Process Equipment and Plant Design
The shell side pressure drop in a shell and tube heat exchanger is maximum for __________ baffle.

Segmental
Orifice
Disk and ring
Independent of the type of

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